To describe the effects of turbulent fluctuations of velocities and scalar quantities in a single phase, FLUENT uses various types of closure models, as described in Chapter 12. In comparison to single-phase flows, the number of terms to be modeled in the momentum equations in multiphase flows is large, and this makes the modeling of turbulence in multiphase simulations extremely complex.
FLUENT provides three methods for modeling turbulence in multiphase flows within the context of the - models. In addition, FLUENT provides two turbulence options within the context of the Reynolds stress models (RSM).
The - turbulence model options are:
| Note that the descriptions of each method below are presented based on the standard
model. The multiphase modifications to the RNG and realizable
models are similar, and are therefore not presented explicitly.
The RSM turbulence model options are:
For either category, the choice of model depends on the importance of the secondary-phase turbulence in your application.
- Turbulence Models
FLUENT provides three turbulence model options in the context of the - models: the mixture turbulence model (the default), the dispersed turbulence model, or a per-phase turbulence model.
- Mixture Turbulence Model
The mixture turbulence model is the default multiphase turbulence model. It represents the first extension of the single-phase - model, and it is applicable when phases separate, for stratified (or nearly stratified) multiphase flows, and when the density ratio between phases is close to 1. In these cases, using mixture properties and mixture velocities is sufficient to capture important features of the turbulent flow.
The and equations describing this model are as follows:
where the mixture density and velocity, and , are computed from
the turbulent viscosity, , is computed from
and the production of turbulence kinetic energy, , is computed from
The constants in these equations are the same as those described in Section 12.4.1 for the single-phase - model.
- Dispersed Turbulence Model
The dispersed turbulence model is the appropriate model when the concentrations of the secondary phases are dilute. In this case, interparticle collisions are negligible and the dominant process in the random motion of the secondary phases is the influence of the primary-phase turbulence. Fluctuating quantities of the secondary phases can therefore be given in terms of the mean characteristics of the primary phase and the ratio of the particle relaxation time and eddy-particle interaction time.
The model is applicable when there is clearly one primary continuous phase and the rest are dispersed dilute secondary phases.
The dispersed method for modeling turbulence in FLUENT assumes the following:
Turbulent predictions for the continuous phase are obtained using the standard - model supplemented with extra terms that include the interphase turbulent momentum transfer.
Predictions for turbulence quantities for the dispersed phases are obtained using the Tchen theory of dispersion of discrete particles by homogeneous turbulence [ 142].
In turbulent multiphase flows, the momentum exchange terms contain the correlation between the instantaneous distribution of the dispersed phases and the turbulent fluid motion. It is possible to take into account the dispersion of the dispersed phases transported by the turbulent fluid motion.
The choice of averaging process has an impact on the modeling of dispersion in turbulent multiphase flows. A two-step averaging process leads to the appearance of fluctuations in the phase volume fractions. When the two-step averaging process is used with a phase-weighted average for the turbulence, however, turbulent fluctuations in the volume fractions do not appear. FLUENT uses phase-weighted averaging, so no volume fraction fluctuations are introduced into the continuity equations.
Turbulence in the Continuous Phase
The eddy viscosity model is used to calculate averaged fluctuating quantities. The Reynolds stress tensor for continuous phase takes the following form:
where is the phase-weighted velocity.
The turbulent viscosity is written in terms of the turbulent kinetic energy of phase :
and a characteristic time of the energetic turbulent eddies is defined as
where is the dissipation rate and .
The length scale of the turbulent eddies is
Turbulent predictions are obtained from the modified - model:
Here and represent the influence of the dispersed phases on the continuous phase , and is the production of turbulent kinetic energy, as defined in Section 12.4.4. All other terms have the same meaning as in the single-phase - model.
The term can be derived from the instantaneous equation of the continuous phase and takes the following form, where represents the number of secondary phases:
which can be simplified to
where is the covariance of the velocities of the continuous phase and the dispersed phase (calculated from Equation 23.5-109 below), is the relative velocity, and is the drift velocity (defined by Equation 23.5-114 below).
is modeled according to Elgobashi et al. [ 97]:
Turbulence in the Dispersed Phase
Time and length scales that characterize the motion are used to evaluate dispersion coefficients, correlation functions, and the turbulent kinetic energy of each dispersed phase.
The characteristic particle relaxation time connected with inertial effects acting on a dispersed phase is defined as
The Lagrangian integral time scale calculated along particle trajectories, mainly affected by the crossing-trajectory effect [ 70], is defined as
where is the angle between the mean particle velocity and the mean relative velocity. The ratio between these two characteristic times is written as
Following Simonin [ 334], FLUENT writes the turbulence quantities for dispersed phase as follows:
and is the added-mass coefficient.
Interphase Turbulent Momentum Transfer
The turbulent drag term for multiphase flows ( in Equation 23.5-7) is modeled as follows, for dispersed phase and continuous phase :
The second term on the right-hand side of Equation 23.5-113 contains the drift velocity:
Here and are diffusivities, and is a dispersion Prandtl number. When using Tchen theory in multiphase flows, FLUENT assumes and the default value for is 0.75.
The drift velocity results from turbulent fluctuations in the volume fraction. When multiplied by the exchange coefficient , it serves as a correction to the momentum exchange term for turbulent flows. This correction is not included, by default, but you can enable it during the problem setup.
You can enable the effect of drift velocity by performing the following:
define models viscous multiphase-turbulence multiphase-options
/define/models/viscous/multiphase-turbulence> multiphase-options Enable dispersion force in momentum? [no] yes Enable interphase k-epsilon source? [no] yes
The effect of the drift velocity is influenced both by the momentum equation and, to a lesser extent, the turbulence equation. Therefore, you should answer yes to both questions to take into account the effect of drift velocity.
- Turbulence Model for Each Phase
The most general multiphase turbulence model solves a set of and transport equations for each phase. This turbulence model is the appropriate choice when the turbulence transfer among the phases plays a dominant role.
Note that, since FLUENT is solving two additional transport equations for each secondary phase, the per-phase turbulence model is more computationally intensive than the dispersed turbulence model.
The Reynolds stress tensor and turbulent viscosity are computed using Equations 23.5-94 and 23.5-95. Turbulence predictions are obtained from
The terms and can be approximated as
where is defined by Equation 23.5-107.
Interphase Turbulent Momentum Transfer
The turbulent drag term ( in Equation 23.5-7) is modeled as follows, where is the dispersed phase (replacing in Equation 23.5-7) and is the continuous phase:
Here and are phase-weighted velocities, and is the drift velocity for phase (computed using Equation 23.5-114, substituting for ). Note that FLUENT will compute the diffusivities and directly from the transport equations, rather than using Tchen theory (as it does for the dispersed turbulence model).
As noted above, the drift velocity results from turbulent fluctuations in the volume fraction. When multiplied by the exchange coefficient , it serves as a correction to the momentum exchange term for turbulent flows. This correction is not included, by default, but you can enable it during the problem setup.
The turbulence model for each phase in FLUENT accounts for the effect of the turbulence field of one phase on the other(s). If you want to modify or enhance the interaction of the multiple turbulence fields and interphase turbulent momentum transfer, you can supply these terms using user-defined functions.
RSM Turbulence Models
Multiphase turbulence modeling typically involves two equation models that are based on single-phase models and often cannot accurately capture the underlying flow physics. Additional turbulence modeling for multiphase flows is diminished even more when the basic underlying single-phase model cannot capture the complex physics of the flow. In such situations, the logical next step is to combine the Reynolds stress model with the multiphase algorithm in order to handle challenging situations in which both factors, RSM for turbulence and the Eulerian multiphase formulation, are a precondition for accurate predictions [ 66].
The phase-averaged continuity and momentum equations for a continuous phase are:
For simplicity, the laminar stress-strain tensor and other body forces such as gravity have been omitted from Equations 23.5-119- 23.5-120. The tilde denotes phase-averaged variables while an overbar (e.g., ) reflects time-averaged values. In general, any variable can have a phase-average value defined as
Considering only two phases for simplicity, the drag force between the continuous and the dispersed phases can be defined as:
where is the drag coefficient. Several terms in the Equation 23.5-122 need to be modeled in order to close the phase-averaged momentum equations. Full descriptions of all modeling assumptions can be found in [ 65]. This section only describes the different modeling definition of the turbulent stresses that appears in Equation 23.5-120.
The turbulent stress that appears in the momentum equations need to be defined on a per-phase basis and can be calculated as:
where the subscript is replaced by for the primary (i.e., continuous) phase or by for any secondary (i.e., dispersed) phases. As is the case for single-phase flows, the current multiphase Reynolds stress model (RSM) also solves the transport equations for Reynolds stresses . FLUENT includes two methods for modeling turbulence in multiphase flows within the context of the RSM model: the dispersed turbulence model, and the mixture turbulence model.
RSM Dispersed Turbulence Model
The dispersed turbulence model is used when the concentrations of the secondary phase are dilute and the primary phase turbulence is regarded as the dominant process. Consequently, the transport equations for turbulence quantities are only solved for the primary (continuous) phase, while the predictions of turbulence quantities for dispersed phases are obtained using the Tchen theory. The transport equation for the primary phase Reynolds stresses in the case of the dispersed model are:
The variables in Equation 23.5-124 are per continuous phase and the subscript is omitted for clarity. The last term of Equation 23.5-124, , takes into account the interaction between the continuous and the dispersed phase turbulence. A general model for this term can be of the form:
where and are unknown coefficients, is the relative velocity, represents the drift or the relative velocity, and is the unknown particulate-fluid velocity correlation. To simplify this unknown term, the following assumption has been made:
where is the Kronecker delta, and represents the modified version of the original Simonin model [ 334].
where represents the turbulent kinetic energy of the continuous phase, is the continuous-dispersed phase velocity covariance and finally, and stand for the relative and the drift velocities, respectively. In order to achieve full closure, the transport equation for the turbulent kinetic energy dissipation rate ( ) is required. The modeling of together with all other unknown terms in Equation 23.5-127 are modeled in the same way as in [ 65].
RSM Mixture Turbulence Model
The main assumption for the mixture model is that all phases share the same turbulence field which consequently means that the term in the Reynolds stress transport equations (Equation 23.5-124) is neglected. Apart from that, the equations maintain the same form but with phase properties and phase velocities being replaced with mixture properties and mixture velocities. The mixture density, for example, can be expressed as
while mixture velocities can be expressed as
where is the number of species.